CN106784943B - A kind of membrane electrode of fuel batter with proton exchange film of high power density and preparation method thereof - Google Patents
A kind of membrane electrode of fuel batter with proton exchange film of high power density and preparation method thereof Download PDFInfo
- Publication number
- CN106784943B CN106784943B CN201611177018.4A CN201611177018A CN106784943B CN 106784943 B CN106784943 B CN 106784943B CN 201611177018 A CN201611177018 A CN 201611177018A CN 106784943 B CN106784943 B CN 106784943B
- Authority
- CN
- China
- Prior art keywords
- carbon
- proton exchange
- membrane electrode
- power density
- carbon nanotube
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Active
Links
Classifications
-
- H—ELECTRICITY
- H01—ELECTRIC ELEMENTS
- H01M—PROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
- H01M8/00—Fuel cells; Manufacture thereof
- H01M8/10—Fuel cells with solid electrolytes
- H01M8/1004—Fuel cells with solid electrolytes characterised by membrane-electrode assemblies [MEA]
-
- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02E—REDUCTION OF GREENHOUSE GAS [GHG] EMISSIONS, RELATED TO ENERGY GENERATION, TRANSMISSION OR DISTRIBUTION
- Y02E60/00—Enabling technologies; Technologies with a potential or indirect contribution to GHG emissions mitigation
- Y02E60/30—Hydrogen technology
- Y02E60/50—Fuel cells
Landscapes
- Life Sciences & Earth Sciences (AREA)
- Engineering & Computer Science (AREA)
- Manufacturing & Machinery (AREA)
- Sustainable Development (AREA)
- Sustainable Energy (AREA)
- Chemical & Material Sciences (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Electrochemistry (AREA)
- General Chemical & Material Sciences (AREA)
- Fuel Cell (AREA)
- Inert Electrodes (AREA)
Abstract
The invention discloses membrane electrode of fuel batter with proton exchange film of a kind of high power density and preparation method thereof.This method is the thickness by reducing solid electrolyte, use high-content catalyst degradation catalyst layer thickness, and the mass transfer of carbon nanotubes or carbon fiber improvement catalyst layer and diffusion layer is introduced in cathode catalysis layer and/or gas diffusion layers, so that the power density of membrane electrode is greatly improved.Preparation method step of the present invention is simple, practical easy, low in cost；The thickness that membrane electrode can be reduced while improving membrane electrode performance, is conducive to the preparation of high power density fuel cell, pile and system.
Description
Technical field
The present invention relates to Proton Exchange Membrane Fuel Cells fields, and in particular to cathode catalysis layer or cathode gas diffusion layer contain
There is the high power density membrane electrode and preparation method thereof of hydrophilic carbon nano tube or azotized carbon nano pipe.
Background technique
Proton Exchange Membrane Fuel Cells (PEMFC) is a kind of new green energy technology, it have energy conversion efficiency it is high,
The advantages that cold-starting is quick, pollution-free is with a wide range of applications on automobile power and small portable generating equipment.
Research in relation to PEMFC has become the hot subject in the fields such as green energy resource, and many developed countries are all competitively developing this
Technology.
Membrane electrode of fuel batter with proton exchange film is mainly by male/female pole Catalytic Layer, male/female pole gas diffusion layers and Nafion
Proton exchange membrane composition.It is well known that the microstructure of Catalytic Layer is the slurry by being coated in proton exchange membrane in membrane electrode
It is determined, and the composition of slurry and degree of scatter are to the migration velocity and reactant of catalyst utilization, proton and the expansion of product
It dissipates and has a great impact.Currently, common Catalytic Layer the preparation method comprises the following steps: by catalyst, binder and dispersant configure
At slurries, the grout distribution is then formed into Catalytic Layer in the two sides of proton exchange membrane in the method for coating, transfer or spraying.Often
The cathode catalysis layer of rule method preparation is unfavorable for the transmission of the utilization of catalyst, reactants and products, to reduce battery
Performance.The diffusion transport of reactants and products affects battery performance, the preparation method of common diffusion layer in gas diffusion layers
Are as follows: carbon dust and binder are dispersed in alcohol solvent, ultrasonic disperse is configured to slurries, and the slurries are then passed through blade coating or spray
Coating method is supported on carbon paper or the side of carbon cloth forms diffusion layer.The diffusion layer of conventional method preparation is unfavorable for reactants and products
Diffusion to block duct, and then reduce battery performance.Catalytic Layer and gas diffusion layers can all be carried out with reactants and products
Contact, structure and performance all have a great impact to the output performance and power density of battery.
Chinese patent ZL201410568683.0 discloses " a kind of preparation method of hydrogen fuel cell membrane electrode ", the patent
It proposes that pore creating material (ammonium hydrogen carbonate, ammonium oxalate, sodium chloride etc.) is added in conventional catalysis layer material, pore creating material is in heat resolve
Certain hole is formed in the process, improves the pore-size distribution of membrane electrode, reduces gas transfer resistance.
Chinese patent ZL201310333544.5 discloses " membrane electrode and preparation method thereof for fuel cell ", this is specially
Benefit application increases thickener (glycerine, ethylene glycol, butyl acetate etc.) and additive (carbonic acid in conventional catalyst slurry
Hydrogen ammonium, ammonium acetate, dimethicone etc.), wherein thickener dielectric constant with higher and viscosity, the bicarbonate in additive
Ammonium and ammonium acetate are pore creating material, can equally increase the porosity of Catalytic Layer, and it is anti-at higher current densities to improve cathode catalysis layer
Answer the transmission of object and product.But the pore creating material being introduced into this method generates toxic gas, and pore creating material heat in pyrolytic process
Solution can be not exclusively trapped in Catalytic Layer, increased so as to cause the contact resistance of Catalytic Layer, reduced battery performance.
Chinese patent ZL200710019376.7 discloses " preparation method of fuel battery gas diffusion layer ", which mentions
Go out and carbon paper or carbon cloth have been put by carbon black powder (acetylene black or active carbon black), distilled water, PTFE or PVDF lotion, dispersing agent
It is impregnated 0.5-15 minutes in the slurries of (XH-1, AEO-9, FC4430, Tween-60 or Triton X-100) composition, takes out and dry
Dry, above step is until obtain the required carbon paper or carbon cloth for being loaded with carbon black and PTFE or PVDF repeatedly.The gas of this method preparation
Body diffused layer structure is more stable, is suitble to the large-scale production of fuel cell.But slurries are easily dispersed in gas diffusion layers in this method
The two sides and inside of substrate are unfavorable for controlling product quality, and the microporous layers prepared contact insecure with substrate, can bring battery
The shortcomings that internal resistance increases, and battery performance reduces.
Chinese patent ZL201210197913.8 discloses " ordering single electrode and membrane electrode based on 3 dimension proton conductors
And preparation method ", which proposes a kind of ordering membrane electrode, using the 3 dimension proton conductors with nanofiber array as substrate,
Proton conductor nanofiber array is grown in the two sides of proton exchange membrane, and uniformly plates urging for one layer of active metal on array
Change layer.The contact area that will increase film and Catalytic Layer with membrane electrode prepared by this method, is conducive to the diffusion of reactants and products,
Accelerate proton transport.But the membrane electrode of this method preparation ordering structure in assembling bonding processes can meet with due to the effect of pressure
To destruction, the fuel cell after assembling loses ordering structure, is unfavorable for the diffusion of reactants and products, while reducing catalysis
The utilization efficiency of agent.
Chinese patent ZL201080019534.9 discloses " gas diffusion layer for fuel cell ", and the patent proposes in gas
Setting has the water wetted material (active carbon, zeolite, silica gel, aluminium oxide etc.) of micropore in body diffused layer, and this method is by making to react
The water being trapped in cathode catalysis layer in the process diffuses in the gas diffusion layers with water-absorbent material, can prevent due in low temperature
Product hinders the diffusion phenomena of reactant caused by the freezing of cathode catalysis layer during operation, thus improves battery in low temperature
Starting ability under environment.But the addition of water-absorbent material will increase the stagnation amount of the water in gas diffusion layers, can equally hinder anti-
Answer object in the distribution and diffusion of gas diffusion layers, and the addition of dielectric water-absorbent material will increase the internal resistance of fuel cell,
It is unfavorable for the raising of battery performance.
Chinese patent ZL201010567204.5 disclose " for Proton Exchange Membrane Fuel Cells cathode diffusion layer and its
Preparation and application ", which increases 5%-10% hydrogen-storing material (CeO in conventional diffusion layer slurry2、ZrO2、TiO2、
SnO2、InO2、Sb2O5Deng), which has stronger oxygen transfer capacity, is used for cathode gas diffusion layer, battery
Performance significantly improves.But the hydrogen-storing material electric conductivity in this method is very poor even without electric conductivity, CeO2Deng storage oxygen material
The shortcomings that introducing of material can bring internal resistance to increase.
Chinese patent ZL201410521061.2 discloses " a kind of preparation method of the electrode suitable for fuel cell ", should
Patent proposes that carbon nanotube or carbon nano-fiber are added in conventional microporous layer material, with the method for wet process or dry method formation one
Layer microporous layer, the microporous layer are able to achieve reallocation of the reactants and products in membrane electrode.The patent is also proposed to be added and be made
Hole agent, the pore-size distribution of the adjustable microporous layer of pore creating material, improves the mass-transfer performance of microporous layer, to effectively improve battery
Output performance.
Although the effect that the method for above-mentioned report has degree different in the aspect of performance for promoting membrane electrode, current
The power density of fuel cell membrane electrode is still relatively low, and the fuel cell system with the highly compacts such as electric car is to membrane electrode
The requirement of power density still has huge gap.Therefore, the membrane electrode that preparation has higher power density is further explored
And its technology of preparing still has a very important significance.
Summary of the invention
In order to solve defect existing for existing the relevant technologies and deficiency, the invention proposes a kind of protons of high power density
Exchange film fuel cell film electrode and preparation method thereof, by adding suitable substance and optimization in Catalytic Layer and gas diffusion layers
Fabrication Technology of Electrode, Catalytic Layer obtained and gas diffusion layers have high-specific surface area, high catalyst degrees of exposure and significantly mention
High reactants and products diffusion transport ability, so that the power density of membrane electrode obtained is greatly improved.
The purpose of the present invention is realized at least through one of following technical solution.
A kind of preparation method of the membrane electrode of fuel batter with proton exchange film of high power density, includes the following steps:
(1) proton exchange membrane is successively aoxidized with hydrogen peroxide, sulfuric acid, acidizing pretreatment, is subsequently placed in deionized water
In save backup；In use, taking out proton exchange membrane, surface moisture is blotted, is fixed in special tooling for coating sun
Pole and cathode catalysis layer；The proton exchange membrane is copolymer solid electrolyte with different thickness；
(2) carbon nanotube or carbon fiber are pre-processed；
(3) by the alloy catalyst of carbon supported platinum catalyst or platinum and other metals, perfluorinated sulfonic acid polymer, by locating in advance
After the carbon nanotube or carbon fiber and volatile solvents of reason are by the mass ratio mixing of 10:2-5:0-5:200-2000, warp
Ink shape slurry is made after ultrasonic disperse processing in 0.5-2 hours, then is coated the ink shape slurry using spraying or brush coating process
In the side of proton exchange membrane, the carrying capacity of Pt is controlled in 0.1-1mg cm-2Between, it then will coat the proton exchange of Catalytic Layer
Film is heat-treated 20-60 minutes at 50-80 DEG C, obtains the cathode catalysis layer containing carbon nanotube；
(4) by the catalyst of carbon supported platinum catalyst or platinum and other metal alloys, perfluorinated sulfonic acid polymer and volatile
Property solvent by 10:2-5:200-2000 mass ratio mixing after, be dispersed into after ultrasonic oscillation within 0.5-2 hour ink shape starch
The slurry, is sprayed on the other side of the proton exchange membrane after step (3) processing by material, and the carrying capacity of Pt is controlled in 0.05-
0.4mg cm-2Between, the proton exchange membrane sprayed is toasted 20-60 minutes at 50-80 DEG C then, membrane electrode is made
Anode catalyst layer；
It completes that anode catalyst layer and cathode catalysis layer is respectively coated on proton exchange membrane two sides, obtains as three-in-one film electricity
Pole；
(5) carbon paper is subjected to hydrophobic treatment；
(6) XC-72 carbon dust, ptfe emulsion, carbon nanotube or carbon fiber and volatile solvents are pressed into 10:1-4:
The mass ratio of 0-5:200-2000 mixes, and ultrasonic disperse 30-80 minutes, ink shape slurry is made, using spraying and brush coating process
The slurry is coated to the side of the carbon paper by silicic acid anhydride, the carrying capacity control of carbon dust, carbon nanotube or carbon fiber exists
2.4-3.4 mg cm-2, the carbon paper sprayed is toasted 20-60 minutes at 50-80 DEG C, is roasted at 340-430 DEG C after dry
0.5-2 hours, cathode gas diffusion layer is made；The mass percent concentration of the ptfe emulsion is 10-25 wt%；
(7) XC-72 carbon dust, ptfe emulsion and volatile solvents are pressed to the mass ratio of 10:1-4:200-2000
Mixing, ultrasonic disperse 30-80 minute obtained ink shape slurries, by the slurry using spraying or brushing method be coated to by
The side of the carbon paper of silicic acid anhydride toasts the carbon paper sprayed 20-60 minutes at 50-80 DEG C, in 340-430 after drying
It is roasted 0.5-2 hours at DEG C, anode gas diffusion layer is made；The mass percent concentration of the ptfe emulsion is 10-
25 wt%；
(8) two gas diffusion layers after handling through (6) and (7) are fitted in respectively to be closed through made from step (4) three
Then the corresponding side of one membrane electrode, 110-150 degree hot pressing 3-5 minutes carry out edge sealing processing；Obtain cathode catalysis layer or
Gas diffusion layers contain the five in one membrane electrode (such as Fig. 1) of carbon nanotube.When small area is tested, it can also save at hot pressing and edge sealing
Manage step.
A kind of membrane electrode of fuel batter with proton exchange film of high power density, the membrane electrode are starched in cathod catalyst
Carbon nanotube is introduced in material or cathode gas diffusion layer or carbon fibre material is prepared.
Further, the carbon nanotube and carbon fibre material include untreatment carbon nanotube or carbon fiber, acid processing
One of carbon nanotube or carbon fiber, azotized carbon nano pipe or carbon fiber or more than one.
Further, the proton exchange membrane is the Hydrogen Proton exchange membrane that thickness is respectively 20 to 50 microns, including
But it is not limited to Nafion212, Nafion211 film etc. of DuPont's production.
Further, used the catalyst of high platinum content, catalyst be the Pt/C that Pt content is 20% -60% or
PtM/C catalyst, wherein M is Ru, Pd or Au；The including but not limited to catalyst of Johanson Matthey company.
Further, the perfluorinated sulfonic acid polymer is added in the form of perfluorinated sulfonic acid polymer solution, the perfluor sulphur
Acid polymer solution is the Nafion solution that mass percentage concentration is 2-5% or so.
Further, the volatile solvents are one or more of distilled water, ethyl alcohol or isopropanol.
Further, in step (2), the pretreatment of carbon nanotube or carbon fiber is handled including acid or nitrogen treatment, at acid
Reason and two kinds of processing methods of nitrogen treatment；
Wherein the acid processing or nitridation process step are as follows:
Carbon nanometer or carbon fiber pipe are put into the concentrated sulfuric acid/concentrated nitric acid solution of volume ratio 2.5-3:1 and are ultrasonically treated 20-30
Minute, 60-90 DEG C reflux 6-12 hours, filter and be washed with deionized carbon nanotube or carbon fiber to neutrality, that is, obtain
Acid processing carbon nanotube or carbon fiber.
Carbon nanotube or carbon fiber are put into quartz tube furnace, temperature program is adjusted, the flow velocity for controlling ammonia is 60-
150 ml/mins, 700-900 DEG C roasting 0.5-3 hours, then drop to room temperature, change ammonia into nitrogen or argon gas, with
Ammonia in removing system takes out sample, i.e. acquisition azotized carbon nano pipe；
The acid processing and nitridation process step are as follows:
Carbon nanometer or carbon fiber pipe are put into the concentrated sulfuric acid/concentrated nitric acid solution of volume ratio 2.5-3:1 and are ultrasonically treated 20-30
Minute, 60-90 DEG C reflux 6-12 hours, filter and be washed with deionized carbon nanotube or carbon fiber to neutrality, that is, obtain
Acid processing carbon nanotube or carbon fiber.
It will be put into quartz tube furnace through peracid treatment carbon nanotube or carbon fiber, and adjust temperature program, control ammonia
Flow velocity be 60-150 ml/min, 700-900 DEG C roasting 0.5-3 hours, then drop to room temperature, change ammonia into nitrogen
Or argon gas takes out sample with the ammonia in removing system, that is, obtains azotized carbon nano pipe.
Further, carbon nanotube or carbon fiber, the carbon nanotube are added in catalyst layer and gas diffusion layers
Or carbon nano-fiber be untreatment carbon nanotube or carbon fiber, acid processing carbon nanotube or carbon fiber and azotized carbon nano pipe or
Person's carbon fiber, additive amount are the 5-50% of Catalytic Layer or gas diffusion layers gross mass.
Further, the detailed process of step (1) are as follows: pair for being 5%-15% by proton exchange membrane merging mass percentage concentration
It in oxygen water, is boiled at 60-100 DEG C 0.5-2 hours, after distilling water washing, then is put in 0.5-1mol L-1Sulfuric acid solution in,
It is boiled at 60-100 DEG C 0.5-2 hours, is then washed with distilled water clean, i.e. completion pretreatment.
Further, in step (5), detailed process are as follows: it is small that TGP-H-60 carbon paper is placed in processing 0.5-2 in acetone
When, to remove surface organic matter impurity, 2- is impregnated in the ptfe emulsion that mass percentage concentration is 5%-15% after dry
15 minutes, dry, polytetrafluoroethylene (PTFE) accounts for the 10%-25% of whole carbon paper weight, and it is small that 0.5-2 is roasted at 300-500 DEG C
When, it is sintered polytetrafluoroethylene (PTFE) in carbon paper, that is, completes the hydrophobic treatment of carbon paper.
Compared with prior art, the present invention having the advantage that
1. carbon nanotube of the present invention is that direct addition is starched in cathode inks or cathode gas diffusion layer
In material, the diffusion of reactant and the benefit of cathod catalyst can be effectively improved by introducing carbon nanotube or carbon fiber in cathode catalysis layer
With efficiency, the diffusion of reactants and products can be effectively improved by introducing carbon nanotube or carbon fiber in cathode diffusion layer, to mention
The battery performance in high high current density area；
2. the high power density capability of membrane electrode prepared by the present invention is embodied in: in high current density region, cathode catalysis
The water that layer generates can diffuse quickly into gas diffusion layers and be discharged, while accelerating reaction gas to be transferred in Catalytic Layer and participating in
Reaction, to achieve the purpose that improve cell output.
3. preparation method is simple for high power density membrane electrode of the present invention, does not need special instrument and set
It is standby, it is low in cost, it can be mass-produced；
4. it is functional using the monocell that membrane electrode of the present invention is assembled, in low current density area, performance
Higher than the common battery performance for being not added with carbon nanotube or carbon fiber；In high current density region, performance is even substantially better than
The performance of carbon nanotube or carbon fiber battery is not added.
Detailed description of the invention
Fig. 1 is the five in one film electrode structure schematic diagram for adding carbon nanotube；
Fig. 2 (a) is 212 film of blank electricity prepared by membrane electrode prepared by embodiment 1 to embodiment 3 and comparative example 1
211 membrane electrode of blank prepared by pole and comparative example 2 is 70 degree in hydrogen-air cell temperature, and anode and cathode back pressure is
30psi, relative humidity are the monocell polarization curve comparison diagram under 100%；
Fig. 2 (b) is 212 film of blank electricity prepared by membrane electrode prepared by embodiment 1 to embodiment 3 and comparative example 1
211 membrane electrode of blank prepared by pole and comparative example 2 is 70 degree in hydrogen-air cell temperature, and anode and cathode back pressure is
30psi, relative humidity are the monocell power density comparison diagram under 100%；
Fig. 3 (a) is 212 film of blank electricity prepared by membrane electrode prepared by embodiment 4 to embodiment 6 and comparative example 1
211 membrane electrode of blank prepared by pole and comparative example 2 is 70 degree in hydrogen-air-fuel battery temperature, anode and cathode back pressure
For 30psi, relative humidity is the monocell polarization curve comparison diagram under 100%；
Fig. 3 (b) is 212 film of blank electricity prepared by membrane electrode prepared by embodiment 4 to embodiment 6 and comparative example 1
211 membrane electrode of blank prepared by pole and comparative example 2 is 70 degree in hydrogen-air fuel cell temperature, and anode and cathode back pressure is
30psi, relative humidity are the monocell power density comparison diagram under 100%；
Fig. 4 (a) be embodiment 2,5,7 prepare membrane electrode and comparative example 1 prepared by 212 membrane electrode of blank and
211 membrane electrode of blank prepared by comparative example 2 is 70 degree in hydrogen-air fuel cell temperature, and anode and cathode back pressure is 30psi,
Relative humidity is the monocell polarization curve comparison diagram under 100%；
Fig. 4 (b) be embodiment 2,5,7 prepare membrane electrode and comparative example 1 prepared by 212 membrane electrode of blank and
211 membrane electrode of blank prepared by comparative example 2 is 70 degree in hydrogen-air fuel cell temperature, and anode and cathode back pressure is 30psi,
Relative humidity is the monocell power density comparison diagram under 100%.
All parts are as follows in Fig. 1: proton exchange membrane 1, anode catalyst layer 2, cathode catalysis layer 3, anode gas diffusion layer
Microporous layers 4.1, the microporous layers of cathode gas diffusion layer 4.2, carbon paper 5；The wherein microporous layers 4.1 and carbon of anode gas diffusion layer
Paper 5 is anode gas diffusion layer, and the microporous layers 4.2 and carbon paper 5 of cathode gas diffusion layer are cathode gas diffusion layer.
Specific embodiment
The object of the invention will be described in further detail in the following with reference to the drawings and specific embodiments, and embodiment is not
It can repeat one by one herein, but therefore embodiments of the present invention are not limited to the following examples.Unless stated otherwise, of the invention
The material and processing method used is the art conventional material and processing method.
Embodiment 1
The first step takes the Nafion211 proton exchange membrane of 4cm × 4cm, is initially positioned at the dioxygen that mass percentage concentration is 5%
It is handled 1 hour for 80 DEG C in water, after distilling water washing, in 0.5mol L-1Sulfuric acid solution in handle 1 hour at 80 DEG C, then use
Distilled water washes clean.The Nafion membrane handled well is placed in on the fixed frame for prepare membrane electrode fixed, active region size
For 5cm2, to prevent film contraction distortion during spraying catalyst pulp；
Carbon nanotube is placed in the concentrated sulfuric acid/concentrated nitric acid solution that volume ratio is 3:1 and is ultrasonically treated 30 minutes by second step,
It flows back 8 hours at 80 DEG C, filter and carbon nanotube is washed with deionized to neutrality, that is, obtain acid processing carbon nanotube；
Second step is put into quartz tube furnace by third step through peracid treatment carbon nanotube, adjusts temperature program, controls ammonia
The flow velocity of gas is 120 ml/mins, roasts 2 hours at 900 DEG C, then drops to room temperature, change ammonia into nitrogen or argon gas, with
Ammonia in removing system takes out sample, i.e. acquisition azotized carbon nano pipe；
4th step is weighed the Pt/C catalyst that 4.2 mg Pt contents are 60% by the mass ratio of 10:2.5:1:500 respectively
(Johnson Matthey), 33 mg perfluorinated sulfonic acid polymer solution (5wt% Nafion, DuPont), 0.4 mg carbonitride are received
Mitron and 0.2 g isopropanol, are made catalyst pulp through ultrasonic disperse after mixing, under infrared light irradiation, are sprayed on proton friendship
The side of film is changed, is then heat-treated 30 minutes at 70 DEG C, obtains cathode catalysis layer, wherein the carrying capacity of Pt is 0.2 mg cm-1；
5th step is weighed the Pt/C catalyst that 2.1mg Pt content is 60% by the mass ratio of 10:2.5:500 respectively
(Johnson Matthey), 17 mg perfluorinated sulfonic acid polymer solution (5wt% Nafion, DuPont) and 0.1g isopropanol mix
Through ultrasonic disperse at catalyst pulp after conjunction, under infrared light irradiation, it is sprayed on the proton exchange membrane that the spraying of the 4th step is completed
Then the proton exchange membrane sprayed is heat-treated 30 minutes by the other side at 70 DEG C, the anode catalyst layer of membrane electrode is made,
The carrying capacity of middle Pt is 0.1mg cm-1。
TGP-H-60 carbon paper (Toray company) is cut into the fritter of the cm of 2.5 cm × 2.5 by the 6th step, is placed in third
It is handled 2 hours in ketone, to remove surface organic matter impurity, after drying in the ptfe emulsion that mass percentage concentration is 5%
It impregnates 5 minutes, it is dry, so that polytetrafluoroethylene (PTFE) is accounted for the 15% of whole carbon paper weight, is roasted 1 hour at 500 DEG C, make polytetrafluoroethyl-ne
Alkene is sintered in carbon paper, i.e. the water delivery processing of completion carbon paper.
7th step weighs 30mg XC-72 carbon dust, 132.5mg polytetrafluoroethylene (PTFE) by the mass ratio of 10:1.7:500 respectively
Ink shape slurry is made through ultrasonic disperse after mixing in lotion (mass fraction 5%) and 1.6g aqueous isopropanol, by the pulp spraying
It is coated onto the side of the carbon paper by silicic acid anhydride, the carbon paper sprayed is toasted 30 minutes at 70 DEG C, at 350 DEG C after drying
Under bake 1 hour, be made gas diffusion layers；
Two gas diffusion layers sprayed through the 7th step are fitted in respectively and have sprayed anode and cathode through the 5th step by the 8th step
The two sides of the proton exchange membrane of Catalytic Layer, obtain membrane electrode.(structure is as shown in Figure 1)
Membrane electrode is placed in monocell, is 70 DEG C, under conditions of anode and cathode is humidified completely in battery temperature, is activated
6 hours, electric discharge activated it sufficiently repeatedly, and battery performance test condition is as follows: fuel gas is hydrogen, and oxidant is air,
Battery temperature is 70 DEG C, and anode and cathode back pressure is 30psi, and anode and cathode relative humidity is 100%.
It is 70 DEG C in battery temperature, under conditions of anode and cathode relative humidity is 100%, cell polarization curves such as Fig. 2 a and figure
Shown in 2b, when voltage is 0.7V and 0.6V, current density can respectively reach 700 mA cm-2 With 1300 mA cm-2.It is maximum
Power density is 814 mW cm-2。
Embodiment 2
Carbon supported platinum catalyst, perfluorinated sulfonic acid polymer, azotized carbon nano are weighed except the mass ratio by 10:2.5:2:500
Pipe is with outside isopropanol, other steps are identical as example 1, and cell activation mode and test method are identical with example 1.Battery pole
Change curve as shown in Fig. 2, current density can respectively reach 700 mA cm when voltage is 0.7V and 0.6V-2With 1300 mA
cm-2.Maximum power density is 822 mW cm-2。
Embodiment 3
Carbon supported platinum catalyst, perfluorinated sulfonic acid polymer, azotized carbon nano are weighed except the mass ratio by 10:2.5:3:500
Pipe is with outside isopropanol, other steps are identical as example 1, and cell activation mode and test method are identical with example 1.Battery pole
Change curve as shown in Fig. 2, current density can respectively reach 700 mA cm when voltage is 0.7V and 0.6V-2 With 1250 mA
cm-2.Maximum power density is 780 mW cm-2。
Comparative example 1
The first step takes the Nafion212 proton exchange membrane of 4cm × 4cm, is initially positioned at the dioxygen that mass percentage concentration is 5%
It is handled 1 hour for 80 DEG C in water, after distilling water washing, in 0.5mol L-1Sulfuric acid solution in handle 1 hour at 80 DEG C, then use
Distilled water washes clean.The Nafion membrane handled well is placed in on the fixed frame for prepare membrane electrode fixed, active region size
For 5cm2, to prevent film contraction distortion during spraying catalyst pulp；
Second step is weighed the Pt/C catalyst that 6.4mg Pt content is 40% by the mass ratio of 10:2.5:500 respectively
(Hispec 4100, Johnson Matthey), 50mg perfluorinated sulfonic acid polymer solution (5wt% Nafion, DuPont) and
0.3g isopropanol, is made catalyst pulp through ultrasonic disperse after mixing, under infrared light irradiation, is sprayed on the one of proton exchange membrane
Then side is heat-treated 30 minutes at 70 DEG C, obtains cathode catalysis layer, wherein the carrying capacity of Pt is 0.2mg cm-1；
Third step is weighed the Pt/C catalyst that 3.1mg Pt content is 40% by the mass ratio of 10:2.5:500 respectively
(Hispec4100, Johnson Matthey), 25mg perfluorinated sulfonic acid polymer solution (5wt% Nafion, DuPont) and 0.2g
Catalyst pulp is made through ultrasonic disperse after mixing in isopropanol, under infrared light irradiation, is sprayed on the matter that second step spraying is completed
Then the proton exchange membrane sprayed is heat-treated 30 minutes by the other side of proton exchange at 70 DEG C, the sun of membrane electrode is made
Pole Catalytic Layer, wherein the carrying capacity of Pt is 0.1mg cm-1。
4th step is by TGP-H-60(Toray company) carbon paper is cut into the fritter of the cm of 2.5 cm × 2.5, it is placed in acetone
Middle processing 2 hours is soaked in the ptfe emulsion that mass percentage concentration is 5% after dry with removing surface organic matter impurity
Bubble 5 minutes, it is dry, so that polytetrafluoroethylene (PTFE) is accounted for the 15% of whole carbon paper weight, is roasted 1 hour at 500 DEG C, make polytetrafluoroethylene (PTFE)
It is sintered in carbon paper, i.e. the water delivery processing of completion carbon paper.
5th step weighs 30mg XC-72 carbon dust, 132.5mg polytetrafluoroethylene (PTFE) by the mass ratio of 10:1.7:500 respectively
Ink shape slurry is made through ultrasonic disperse after mixing in lotion (mass fraction 5%) and 1.6g aqueous isopropanol, by the pulp spraying
It is coated onto the side of the carbon paper by silicic acid anhydride, the carbon paper sprayed is toasted 30 minutes at 70 DEG C, at 350 DEG C after drying
Lower roasting 1 hour, is made gas diffusion layers；
Two gas diffusion layers sprayed through the 5th step are fitted in respectively and have sprayed anode and cathode through the 5th step by the 6th step
The two sides of the proton exchange membrane of Catalytic Layer, obtain membrane electrode, are named as 212 membrane electrode of blank.
It is as shown in Figure 2 a and 2 b that polarization performance is tested under test condition same as Example 1, it is relatively wet at 70 DEG C
Under conditions of degree is 100%, when voltage is 0.7V and 0.6V, current density can respectively reach 600 mA cm-2 With 1000 mA
cm-2.Maximum power density is 691 mW cm-2。
Comparative example 2
Except being added without outside carbon nanotube when preparing membrane electrode cathode Catalytic Layer, other preparations, activation and test method are equal
It is same as Example 1.It is named as 211 membrane electrode of blank
Polarization performance is tested under test condition same as Example 1 as shown in Fig. 2, at 70 DEG C, relative humidity is
Under conditions of 100%, when voltage is 0.7V and 0.6V, current density can respectively reach 700 mA cm-2 With 1200 mA cm-2.Maximum power density is 781 mW cm-2。
Embodiment 4
The first step takes the Nafion211 proton exchange membrane of 4cm × 4cm, is initially positioned at the dioxygen that mass percentage concentration is 5%
It is handled 1 hour for 80 DEG C in water, after distilling water washing, in 0.5mol L-1Sulfuric acid solution in handle 1 hour at 80 DEG C, then use
Distilled water washes clean.The Nafion membrane handled well is placed in on the fixed frame for prepare membrane electrode fixed, active region size
For 5cm2, to prevent film contraction distortion during spraying catalyst pulp；
Carbon nanotube is placed in the concentrated sulfuric acid/concentrated nitric acid solution of volume ratio 3:1 and is ultrasonically treated 30 minutes by second step,
80 DEG C are flowed back 8 hours, filter and carbon nanotube is washed with deionized to neutrality, that is, obtain acid processing carbon nanotube.
Second step is put into quartz tube furnace by third step through peracid treatment carbon nanotube, adjusts temperature program, controls ammonia
The flow velocity of gas is 120 ml/mins, roasts 2 hours at 900 DEG C, then drops to room temperature, change ammonia into nitrogen or argon gas, with
Ammonia in removing system takes out sample, i.e. acquisition azotized carbon nano pipe；
4th step is weighed the Pt/C catalyst that 4.2mg Pt content is 60% by the mass ratio of 10:2.5:500 respectively
(Johnson Matthey), 33mg perfluorinated sulfonic acid polymer solution (5wt% Nafion, DuPont) and 0.2g isopropanol, mixing
Catalyst pulp is made by ultrasonic disperse, under infrared light irradiation, the side of proton exchange membrane is sprayed on, then at 70 DEG C
Heat treatment 30 minutes, obtains cathode catalysis layer, and wherein the carrying capacity of Pt is 0.2mg cm-1；
5th step is weighed the Pt/C catalyst that 2.1mg Pt content is 60% by the mass ratio of 10:2.5:500 respectively
(Johnson Matthey), 17mg perfluorinated sulfonic acid polymer solution (5wt% Nafion, DuPont) and 0.1g isopropanol, mixing
Catalyst pulp is made by ultrasonic disperse, under infrared light irradiation, is sprayed on the proton exchange membrane that the spraying of the 4th step is completed
Then the proton exchange membrane sprayed is heat-treated 30 minutes by the other side at 70 DEG C, the anode catalyst layer of membrane electrode is made,
The carrying capacity of middle Pt is 0.1mg cm-1。
6th step is by TGP-H-60(Toray company) carbon paper is cut into the fritter of the cm of 2.5 cm × 2.5, it is placed in third
It is handled 2 hours in ketone, to remove surface organic matter impurity, in the polytetrafluoroethylene (PTFE) that mass percentage concentration is 5%-15% after drying
It is impregnated 5 minutes in lotion, it is dry, so that polytetrafluoroethylene (PTFE) is accounted for the 15% of whole carbon paper weight, is roasted 1 hour at 500 DEG C, make to gather
Tetrafluoroethene is sintered in carbon paper, i.e. the water delivery processing of completion carbon paper.
7th step weighs 30mg XC-72 carbon dust, 132.5mg polytetrafluoroethyl-ne by the mass ratio of 10:1.7:1:500 respectively
Alkene lotion (mass fraction 5%), 3.8mg azotized carbon nano pipe and 1.6g aqueous isopropanol, are made ink through ultrasonic disperse after mixing
The slurry is sprayed to the side of the carbon paper by silicic acid anhydride by watery slurry, and the carbon paper sprayed is toasted at 70 DEG C
It 30 minutes, is roasted 1 hour at 350 DEG C after dry, cathode gas diffusion layer is made；
8th step weighs 30mg XC-72 carbon dust, 132.5mg polytetrafluoroethylene (PTFE) by the mass ratio of 10:1.7:500 respectively
Ink shape slurry is made through ultrasonic disperse after mixing in lotion (mass fraction 5%) and 1.6g aqueous isopropanol, by the pulp spraying
It is coated onto the side of the carbon paper by silicic acid anhydride, the carbon paper sprayed is toasted 30 minutes at 70 DEG C, at 350 DEG C after drying
Lower roasting 1 hour, is made anode gas diffusion layer；
The gas diffusion layers sprayed through the 7th step and the 8th step are fitted in by the 9th step respectively has sprayed yin through the 5th step
The two sides of the proton exchange membrane of anode catalyst layer, obtain membrane electrode.
It is as shown in Figure 3a and Figure 3b shows that polarization performance is tested under test condition same as Example 1, is 0.7V in voltage
When with 0.6V, current density can respectively reach 800 mA cm-2 With 1300 mA cm-2.Maximum power density is 808 mW cm-2。
Embodiment 5
Weighed except the mass ratio by 10:1.7:2:500 XC-72 carbon dust, ptfe emulsion (mass fraction 5%),
Outside azotized carbon nano pipe and isopropanol, other steps are identical as example 4, and cell activation mode and test method and example 4 are completely
It is identical.For cell polarization curves as shown in figure 3, when voltage is 0.7V and 0.6V, current density can respectively reach 800 mA cm-2
With 1300 mA cm-2.Maximum power density is 822 mW cm-2。
Embodiment 6
Weighed except the mass ratio by 10:1.7:3:500 XC-72 carbon dust, ptfe emulsion (mass fraction 5%),
Outside azotized carbon nano pipe and isopropanol, other steps are identical as example 4, and cell activation mode and test method and example 4 are completely
It is identical.For cell polarization curves as shown in figure 3, when voltage is 0.7V and 0.6V, current density can respectively reach 800 mA cm-2
With 1200 mA cm-2.Maximum power density is 730 mW cm-2。
Embodiment 7
The first step takes the Nafion211 proton exchange membrane of 4cm × 4cm, is initially positioned at the dioxygen that mass percentage concentration is 5%
It is handled 1 hour for 80 DEG C in water, after distilling water washing, in 0.5mol L-1Sulfuric acid solution in handle 1 hour at 80 DEG C, then use
Distilled water washes clean.The Nafion membrane handled well is placed in on the fixed frame for prepare membrane electrode fixed, active region size
For 5cm2, to prevent film contraction distortion during spraying catalyst pulp；
Carbon nanotube is put into the concentrated sulfuric acid/concentrated nitric acid solution of volume ratio 3:1 and is ultrasonically treated 30 minutes by second step,
80 DEG C are flowed back 8 hours, filter and carbon nanotube is washed with deionized to neutrality, that is, obtain acid processing carbon nanotube.
Second step is put into quartz tube furnace by third step through peracid treatment carbon nanotube, adjusts temperature program, controls ammonia
The flow velocity of gas is 120 ml/mins, roasts 2 hours at 900 DEG C, then drops to room temperature, change ammonia into nitrogen or argon gas, with
Ammonia in removing system takes out sample, i.e. acquisition azotized carbon nano pipe；
4th step is weighed the Pt/C catalyst that 4.2mg Pt content is 60% by the mass ratio of 10:2.5:2:500 respectively
(Johnson Matthey), 33mg perfluorinated sulfonic acid polymer solution (5wt% Nafion, DuPont), 0.8 mg azotized carbon nano
Pipe and 0.2g isopropanol, are made catalyst pulp through ultrasonic disperse after mixing, under infrared light irradiation, are sprayed on proton exchange membrane
Side, be then heat-treated 30 minutes at 70 DEG C, obtain cathode catalysis layer, wherein the carrying capacity of Pt be 0.2mg cm-1；
5th step is weighed the Pt/C catalyst that 2.1mg Pt content is 60% by the mass ratio of 10:2.5:500 respectively
(Johnson Matthey), 17mg perfluorinated sulfonic acid polymer solution (5wt% Nafion, DuPont) and 0.1g isopropanol, mixing
Catalyst pulp is made by ultrasonic disperse, under infrared light irradiation, is sprayed on the another of the proton exchange membrane of the 4th step completion
Then the proton exchange membrane sprayed is heat-treated 30 minutes by side at 70 DEG C, the anode catalyst layer of membrane electrode is made, wherein Pt
Carrying capacity be 0.1mg cm-1。
6th step is by TGP-H-60(Toray company) carbon paper is cut into the fritter of the cm of 2.5 cm × 2.5, it is placed in third
It is handled 2 hours in ketone, to remove surface organic matter impurity, in the polytetrafluoroethylene (PTFE) that mass percentage concentration is 5%-15% after drying
It is impregnated 5 minutes in lotion, it is dry, so that polytetrafluoroethylene (PTFE) is accounted for the 15% of whole carbon paper weight, is roasted 1 hour at 500 DEG C, make to gather
Tetrafluoroethene is sintered in carbon paper, i.e. the water delivery processing of completion carbon paper.
7th step weighs 30mg XC-72 carbon dust, 132.5mg polytetrafluoroethyl-ne by the mass ratio of 10:1.7:2:500 respectively
Alkene lotion (mass fraction 5%), 7.5mg azotized carbon nano pipe and 1.6g aqueous isopropanol, are made ink through ultrasonic disperse after mixing
The slurry is sprayed to the side of the carbon paper by silicic acid anhydride by watery slurry, and the carbon paper sprayed is toasted at 70 DEG C
It 30 minutes, is roasted 1 hour at 350 DEG C after dry, cathode gas diffusion layer is made；
8th step weighs 30mg XC-72 carbon dust, 132.5mg polytetrafluoroethylene (PTFE) by the mass ratio of 10:1.7:500 respectively
Ink shape slurry is made through ultrasonic disperse after mixing in lotion (mass fraction 5%) and 1.6g aqueous isopropanol, by the pulp spraying
It is coated onto the side of the carbon paper by silicic acid anhydride, the carbon paper sprayed is toasted 30 minutes at 70 DEG C, at 350 DEG C after drying
Lower roasting 1 hour, is made anode gas diffusion layer；
The gas diffusion layers sprayed through the 7th step and the 8th step are fitted in by the 9th step respectively has sprayed yin through the 5th step
The two sides of the proton exchange membrane of anode catalyst layer, obtain membrane electrode.
Polarization performance is tested as shown in figures 4 a and 4b under test condition same as Example 1, it is relatively wet at 70 degree
Under conditions of degree is 100%, when voltage is 0.7V and 0.6V, current density can respectively reach 1000 mA cm-2 With 1600
mA cm-2.Maximum power density is 997 mW cm-2。
Embodiment 8
In addition to using untreatment carbon nanotube replace embodiment 7 in azotized carbon nano pipe other than, membrane electrode preparation step with
And the testing procedure of membrane electrode is all the same as embodiment 7.Above-described embodiment is only presently preferred embodiments of the present invention, is not used to limit this
The practical range of invention.
Under test condition same as Example 7: when voltage is 0.7V and 0.6V, current density can be respectively reached
700 mA cm-2 With 1300 mA cm-2.Maximum power density is 872 mW cm-2。
Embodiment 9
In addition to using acid processing carbon nanotube replace embodiment 7 in azotized carbon nano pipe other than, membrane electrode preparation step with
And the testing procedure of membrane electrode is all the same as embodiment 7.Above-described embodiment is only presently preferred embodiments of the present invention, is not used to limit this
The practical range of invention.
Under test condition same as Example 7: when voltage is 0.7V and 0.6V, current density can be respectively reached
800 mA cm-2 With 1300 mA cm-2.Maximum power density is 872 mW cm-2。
Embodiment 10
Other than the azotized carbon nano pipe replaced in embodiment 7 using nitridation carbon fiber, membrane electrode preparation step and film
The testing procedure of electrode is all the same as embodiment 7.Above-described embodiment is only presently preferred embodiments of the present invention, is not used to limit the present invention
Practical range.
Under test condition same as Example 7: when voltage is 0.7V and 0.6V, current density can be respectively reached
900 mA cm-2 With 1500 mA cm-2.Maximum power density is 926 mW cm-2。
The above embodiment of the present invention be only to clearly illustrate example of the present invention, and not be to the present invention
Embodiment restriction.For those of ordinary skill in the art, it can also make on the basis of the above description
Other various forms of variations or variation.There is no necessity and possibility to exhaust all the enbodiments.It is all of the invention
Made any modifications, equivalent replacements, and improvements etc., should be included in the protection of the claims in the present invention within spirit and principle
Within the scope of.
Claims (10)
1. a kind of preparation method of the membrane electrode of fuel batter with proton exchange film of high power density, which is characterized in that including as follows
Step:
(1) proton exchange membrane is successively aoxidized with hydrogen peroxide, sulfuric acid, acidizing pretreatment, is subsequently placed in deionized water and protects
It deposits spare；In use, taking out proton exchange membrane, blot surface moisture, be fixed in special tooling for coating anode and
Cathode catalysis layer；The proton exchange membrane is copolymer solid electrolyte with different thickness；
(2) carbon nanotube or carbon fiber are pre-processed；
(3) by the alloy catalyst of carbon supported platinum catalyst or platinum and other metals, perfluorinated sulfonic acid polymer, by pretreated
It is small through 0.5-2 after carbon nanotube or carbon fiber and volatile solvents are mixed by the mass ratio of 10:2-5:0-5:200-2000
When ultrasonic disperse processing after be made ink shape slurry, then the ink shape slurry is coated in by proton friendship using spraying or brush coating process
The side of film is changed, the carrying capacity of Pt is controlled in 0.1-1mg cm-2Between, the proton exchange membrane of Catalytic Layer then will have been coated in 50-
It is heat-treated 20-60 minutes at 80 DEG C, obtains the cathode catalysis layer containing carbon nanotube；
(4) catalyst, perfluorinated sulfonic acid polymer and effumability of carbon supported platinum catalyst or platinum and other metal alloys is molten
After agent is by the mass ratio mixing of 10:2-5:200-2000, ink shape slurry is dispersed within 0.5-2 hours after ultrasonic oscillation, it will
The slurry is sprayed on the other side of the proton exchange membrane after step (3) processing, and the carrying capacity of Pt is controlled in 0.05-0.4mg
cm-2Between, then the proton exchange membrane sprayed is toasted 20-60 minutes at 50-80 DEG C, the anode that membrane electrode is made is urged
Change layer；
It completes that anode catalyst layer and cathode catalysis layer is respectively coated on proton exchange membrane two sides, obtains as three in one membreane electrode；
(5) carbon paper is subjected to hydrophobic treatment；
(6) XC-72 carbon dust, ptfe emulsion, carbon nanotube or carbon fiber and volatile solvents are pressed into 10:1-4:0-5:
The mass ratio of 200-2000 mixes, and ultrasonic disperse 30-80 minutes, ink shape slurry is made, should using spraying and brush coating process
Slurry is coated to the side of the carbon paper by silicic acid anhydride, and the carrying capacity of carbon dust, carbon nanotube or carbon fiber is controlled in 2.4-
3.4 mg cm-2, the carbon paper sprayed is toasted 20-60 minutes at 50-80 DEG C, roasts 0.5- at 340-430 DEG C after dry
2 hours, cathode gas diffusion layer is made；The mass percent concentration of the ptfe emulsion is 10-25 wt%；
(7) XC-72 carbon dust, ptfe emulsion and volatile solvents are mixed by the mass ratio of 10:1-4:200-2000
It closes, ultrasonic disperse 30-80 minutes obtained ink shape slurries, which is coated to using spraying or the method brushed by dredging
The side of the carbon paper of hydration process toasts the carbon paper sprayed 20-60 minutes at 50-80 DEG C, at 340-430 DEG C after drying
Anode gas diffusion layer is made in lower roasting 0.5-2 hours；The mass percent concentration of the ptfe emulsion is 10-25
wt%；
(8) two gas diffusion layers after handling through (6) and (7) be fitted in respectively have been sprayed anode and cathode through step (4) and has urged
Change the two sides of the proton exchange membrane of layer, then 110-150 degree hot pressing 3-5 minutes carries out edge sealing processing；Obtain cathode catalysis layer
Or gas diffusion layers contain the five in one membrane electrode of carbon nanotube.
2. the preparation method of the membrane electrode of fuel batter with proton exchange film of high power density according to claim 1, special
Sign is that the proton exchange membrane is the Hydrogen Proton exchange membrane that thickness is respectively 20 to 50 microns.
3. the preparation method of the membrane electrode of fuel batter with proton exchange film of high power density according to claim 1, special
Sign is, has used the catalyst of high platinum content, and catalyst is the Pt/C that Pt content is 20% -60% or PtM/C catalysis
Agent, wherein M is Ru, Pd or Au.
4. the preparation method of the membrane electrode of fuel batter with proton exchange film of high power density according to claim 1, special
Sign is that the perfluorinated sulfonic acid polymer is added in the form of perfluorinated sulfonic acid polymer solution, and the perfluorinated sulfonic acid polymer is molten
Liquid is the Nafion solution that mass percentage concentration is 2-5%.
5. the preparation method of the membrane electrode of fuel batter with proton exchange film of high power density according to claim 1, special
Sign is that the volatile solvents are one or more of distilled water, ethyl alcohol or isopropanol.
6. the preparation method of the membrane electrode of fuel batter with proton exchange film of high power density according to claim 1, special
Sign is, in step (2), the pretreatment of carbon nanotube or carbon fiber is handled including acid or nitrogen treatment, at acid processing and nitridation
Manage two kinds of processing methods；
Wherein the acid processing or nitridation process step are as follows:
Carbon nanometer or carbon fiber pipe are put into the concentrated sulfuric acid/concentrated nitric acid solution of volume ratio 2.5-3:1 and are ultrasonically treated 20-30 points
Clock, 60-90 DEG C reflux 6-12 hours, filter and be washed with deionized carbon nanotube or carbon fiber to neutrality, that is, obtain acid
Handle carbon nanotube or carbon fiber；
Carbon nanotube or carbon fiber are put into quartz tube furnace, temperature program is adjusted, the flow velocity for controlling ammonia is 60-150 milli
Liter/min, 700-900 DEG C roasting 0.5-3 hours, then drop to room temperature, change ammonia into nitrogen or argon gas, be to remove
Ammonia in system takes out sample, i.e. acquisition azotized carbon nano pipe；
The acid processing and nitridation process step are as follows:
Carbon nanometer or carbon fiber pipe are put into the concentrated sulfuric acid/concentrated nitric acid solution of volume ratio 2.5-3:1 and are ultrasonically treated 20-30 points
Clock, 60-90 DEG C reflux 6-12 hours, filter and be washed with deionized carbon nanotube or carbon fiber to neutrality, that is, obtain acid
Handle carbon nanotube or carbon fiber；
It will be put into quartz tube furnace through peracid treatment carbon nanotube or carbon fiber, and adjust temperature program, control the flow velocity of ammonia
For 60-150 ml/min, 700-900 DEG C roasting 0.5-3 hours, then drop to room temperature, change ammonia into nitrogen or argon
Gas takes out sample with the ammonia in removing system, i.e. acquisition azotized carbon nano pipe.
7. the preparation method of the membrane electrode of fuel batter with proton exchange film of high power density according to claim 1, special
Sign is, carbon nanotube or carbon fiber, the carbon nanotube or nano-sized carbon are added in catalyst layer and gas diffusion layers
Fiber is that untreatment carbon nanotube or carbon fiber, acid handle carbon nanotube or carbon fiber and azotized carbon nano pipe or carbon fiber,
Additive amount is the 5-50% of Catalytic Layer or gas diffusion layers gross mass.
8. the preparation method of the membrane electrode of fuel batter with proton exchange film of high power density according to claim 1, special
Sign is the detailed process of step (1) are as follows: is placed in proton exchange membrane in the hydrogen peroxide that mass percentage concentration is 5%-15%, in 60-
It is boiled at 100 DEG C 0.5-2 hours, after distilling water washing, then is put in 0.5-1mol L-1Sulfuric acid solution in, at 60-100 DEG C
It boils 0.5-2 hours, is then washed with distilled water clean, i.e. completion pretreatment.
9. the preparation method of the membrane electrode of fuel batter with proton exchange film of high power density according to claim 1, special
Sign is, in step (5), detailed process are as follows: TGP-H-60 carbon paper is placed in acetone and is handled 0.5-2 hours, to remove surface
Organic impurities impregnate 2-15 minutes in the ptfe emulsion that mass percentage concentration is 5%-15% after dry, dry, gather
Tetrafluoroethene accounts for the 10%-25% of whole carbon paper weight, roasts 0.5-2 hour at 300-500 DEG C, makes polytetrafluoroethylene (PTFE)
It is sintered in carbon paper, that is, completes the hydrophobic treatment of carbon paper.
10. the Proton Exchange Membrane Fuel Cells of high power density is prepared by any one of claim 1 ~ 9 preparation method
Membrane electrode.
Priority Applications (2)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201611177018.4A CN106784943B (en) | 2016-12-19 | 2016-12-19 | A kind of membrane electrode of fuel batter with proton exchange film of high power density and preparation method thereof |
| PCT/CN2017/113215 WO2018113485A1 (en) | 2016-12-19 | 2017-11-27 | Membrane electrode of high power density proton exchange membrane fuel cell and preparation method therefor |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201611177018.4A CN106784943B (en) | 2016-12-19 | 2016-12-19 | A kind of membrane electrode of fuel batter with proton exchange film of high power density and preparation method thereof |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| CN106784943A CN106784943A (en) | 2017-05-31 |
| CN106784943B true CN106784943B (en) | 2019-05-14 |
Family
ID=58889797
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201611177018.4A Active CN106784943B (en) | 2016-12-19 | 2016-12-19 | A kind of membrane electrode of fuel batter with proton exchange film of high power density and preparation method thereof |
Country Status (2)
| Country | Link |
|---|---|
| CN (1) | CN106784943B (en) |
| WO (1) | WO2018113485A1 (en) |
Families Citing this family (58)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN106784943B (en) * | 2016-12-19 | 2019-05-14 | 华南理工大学 | A kind of membrane electrode of fuel batter with proton exchange film of high power density and preparation method thereof |
| CN107437628B (en) * | 2017-07-20 | 2019-09-24 | 河南豫氢动力有限公司 | A kind of preparation method of fuel cell membrane electrode assembly |
| CN107611452A (en) * | 2017-08-15 | 2018-01-19 | 华南理工大学 | A kind of preparation method of the membrane electrode containing three-dimensional hydrophobic cathode catalysis layer |
| CN107482228A (en) * | 2017-08-18 | 2017-12-15 | 福建亚南电机有限公司 | What a kind of anode catalyst was constructed exempts from humidifying film electrode and preparation method thereof |
| CN107634232B (en) * | 2017-09-18 | 2020-06-05 | 大连交通大学 | Preparation method of hydrophobic proton exchange membrane fuel cell membrane electrode |
| CN109524674B (en) * | 2017-09-19 | 2022-06-21 | 粟青青 | Method for improving performance of cathode catalyst layer of membrane electrode of fuel cell |
| CN107681163A (en) * | 2017-09-21 | 2018-02-09 | 上海交通大学 | A kind of fuel cell membrane electrode and its preparation method and application |
| CN109065923A (en) * | 2018-07-06 | 2018-12-21 | 华南理工大学 | Add the high-performance high power density membrane electrode and preparation method thereof of hydrophily carbon material preparation having from humidifying capacity |
| CN109119664B (en) * | 2018-08-28 | 2023-12-12 | 北京林业大学 | Fuel cell based on biomass pyrolysis product and preparation method of membrane electrode |
| CN111038079B (en) * | 2018-10-12 | 2021-11-19 | 浙江森马服饰股份有限公司 | Water-based elastic pyrograph process without adhesive edge |
| CN109524676A (en) * | 2018-11-20 | 2019-03-26 | 安徽明天氢能科技股份有限公司 | A kind of fuel cell catalyst layer electrode of three-dimensional and preparation method thereof |
| CN109713331A (en) * | 2018-12-18 | 2019-05-03 | 新源动力股份有限公司 | A kind of catalyst pulp, catalyst coated membranes, membrane electrode assembly and application thereof |
| CN110247089A (en) * | 2019-07-10 | 2019-09-17 | 浙江博氢新能源有限公司 | Low Pt carrying capacity membrane electrode and preparation method thereof |
| CN110444791A (en) * | 2019-08-28 | 2019-11-12 | 深圳市通用氢能科技有限公司 | Catalyst coat film, fuel cell and preparation method |
| CN110947405B (en) * | 2019-11-08 | 2023-07-28 | 武汉科技大学 | g-C in regular arrangement 3 N 4 Nanotube catalyst and method for preparing same |
| CN111172556B (en) * | 2020-01-02 | 2021-04-20 | 万华化学集团股份有限公司 | Membrane electrode assembly and application thereof in preparing glyoxylic acid through electrochemical reaction |
| CN113140736A (en) * | 2020-06-08 | 2021-07-20 | 上海嘉资新材料有限公司 | Fuel cell gas diffusion layer structure, preparation method, membrane electrode assembly and fuel cell |
| CN114447383A (en) * | 2020-10-31 | 2022-05-06 | 中国石油化工股份有限公司 | Organic-inorganic composite proton exchange membrane and preparation method thereof |
| CN114628701B (en) * | 2020-12-11 | 2024-02-09 | 中国科学院大连化学物理研究所 | Multi-layer catalyst layer, method for the production and use thereof |
| CN112421059B (en) * | 2020-12-15 | 2022-03-22 | 深圳市通用氢能科技有限公司 | Gas diffusion layer and preparation method thereof |
| US12051813B2 (en) | 2020-12-15 | 2024-07-30 | General Hydrogen Corp., Ltd. | Gas diffusion layer and method for preparing same |
| CN112928255B (en) * | 2021-01-25 | 2022-05-06 | 合肥工业大学 | Lithium-sulfur battery composite positive electrode material and preparation method and application thereof |
| CN112993280B (en) * | 2021-03-11 | 2023-11-14 | 大连交通大学 | Preparation method of microporous layer of gas diffusion layer of lithium air battery |
| CN113078338B (en) * | 2021-03-26 | 2022-07-05 | 一汽解放汽车有限公司 | Membrane electrode for fuel cell and preparation method and application thereof |
| CN113233544B (en) * | 2021-05-31 | 2022-09-13 | 青岛大学 | Oil-water separation device and separation method based on PTFE hollow fiber membrane |
| CN113684458B (en) * | 2021-07-06 | 2022-08-12 | 华南理工大学 | Membrane electrode prepared by utilizing multi-wall disordered structure carbon nano tube for proton exchange membrane fuel cell, preparation method and application |
| CN113504285A (en) * | 2021-07-09 | 2021-10-15 | 杭州麦乐克科技股份有限公司 | Preparation method of formaldehyde electrochemical sensor membrane electrode |
| CN113745612A (en) * | 2021-07-30 | 2021-12-03 | 上海唐锋能源科技有限公司 | Membrane electrode with high-efficiency proton transmission network and preparation method thereof |
| CN113991125B (en) * | 2021-10-28 | 2023-07-04 | 一汽解放汽车有限公司 | Proton exchange membrane fuel cell catalyst slurry and preparation method and application thereof |
| CN114068955A (en) * | 2021-10-29 | 2022-02-18 | 浙江天能氢能源科技有限公司 | Fuel cell membrane electrode and preparation method thereof |
| CN114204049B (en) * | 2021-12-03 | 2023-11-10 | 中国科学院大连化学物理研究所 | Preparation method of membrane electrode of proton exchange membrane fuel cell with low platinum loading |
| CN114243034B (en) * | 2021-12-15 | 2023-11-14 | 中国科学院大连化学物理研究所 | Anti-precipitation catalyst slurry and preparation method thereof |
| CN114361479B (en) * | 2021-12-22 | 2024-05-17 | 苏州大学 | High-output power fuel cell and preparation method thereof |
| CN114400335A (en) * | 2022-01-05 | 2022-04-26 | 海南大学 | Preparation method and device of novel two-dimensional patterned electrode |
| CN114512680B (en) * | 2022-01-19 | 2024-03-26 | 东风汽车集团股份有限公司 | Preparation method of proton exchange membrane fuel cell catalytic layer slurry |
| CN114551919B (en) * | 2022-01-24 | 2023-12-19 | 东风汽车集团股份有限公司 | Hydrogel, microporous layer slurry, gas diffusion layer and preparation method of gas diffusion layer |
| CN114524493B (en) * | 2022-01-25 | 2023-04-07 | 中南大学 | Ammonia recovery device and method for electrochemically treating nitrate wastewater |
| CN114705741B (en) * | 2022-02-24 | 2023-07-07 | 南京工业大学 | Method for detecting proton absorption capacity of proton conductor solid oxide fuel cell cathode material in working state |
| CN114540854A (en) * | 2022-03-18 | 2022-05-27 | 中国科学院长春应用化学研究所 | SPEWE membrane electrode and preparation method thereof |
| CN115377448A (en) * | 2022-03-18 | 2022-11-22 | 福州大学 | Application of gas diffusion layer with hydrophilic and hydrophobic structure in fuel cell |
| CN114622245A (en) * | 2022-03-18 | 2022-06-14 | 中国科学院长春应用化学研究所 | Catalyst slurry for water electrolysis hydrogen production and preparation method thereof |
| CN114614061B (en) * | 2022-03-29 | 2023-07-25 | 广州工业智能研究院 | Microbial fuel cell air cathode and preparation method thereof |
| CN114864971B (en) * | 2022-04-14 | 2024-05-17 | 深圳市氢瑞燃料电池科技有限公司 | Fuel cell anti-reverse electrode catalytic layer and preparation method and application thereof |
| CN115020736B (en) * | 2022-04-20 | 2024-01-26 | 中国科学院大连化学物理研究所 | Gas diffusion layer based on fiber arrangement type microporous layer and preparation method and application thereof |
| CN114976048B (en) * | 2022-05-12 | 2024-05-28 | 上海碳际实业集团有限公司 | Continuous production process of special carbon fiber paper for fuel cell gas diffusion layer |
| CN115000420B (en) * | 2022-05-17 | 2024-07-09 | 一汽解放汽车有限公司 | Cathode catalytic membrane, membrane electrode, preparation method of membrane electrode and fuel cell |
| CN115011986A (en) * | 2022-05-25 | 2022-09-06 | 同济大学 | Electrolytic cell membrane electrode with controllable and adjustable pore structure and preparation method and application thereof |
| CN115101765B (en) * | 2022-07-05 | 2024-07-05 | 山西大学 | Method for regulating and controlling membrane electrode catalyst layer by positively charged carbon dots and application of method |
| CN115133043A (en) * | 2022-07-07 | 2022-09-30 | 一汽解放汽车有限公司 | Membrane electrode containing gradient cathode catalyst layer and preparation method and application thereof |
| CN115000446B (en) * | 2022-07-22 | 2024-05-31 | 上海电气集团股份有限公司 | Gas diffusion layer, preparation method thereof, membrane electrode, battery and application |
| CN115084606B (en) * | 2022-08-03 | 2023-07-14 | 上海捷氢科技股份有限公司 | Fuel cell membrane electrode and preparation method and application thereof |
| CN115133048B (en) * | 2022-08-09 | 2024-04-09 | 一汽解放汽车有限公司 | Gas diffusion layer and preparation method and application thereof |
| CN115584046B (en) * | 2022-11-25 | 2023-02-28 | 杭州德海艾科能源科技有限公司 | Perfluorinated sulfonic acid/ketohexose composite ion exchange membrane for vanadium redox battery and preparation method thereof |
| CN116344839B (en) * | 2023-01-13 | 2024-05-28 | 一汽解放汽车有限公司 | High-potential catalyst and preparation method and application thereof |
| CN116845253B (en) * | 2023-06-27 | 2024-01-26 | 哈尔滨工业大学 | Method for regulating and controlling three-phase interface of catalytic layer of proton exchange membrane fuel cell |
| CN117594811A (en) * | 2023-11-16 | 2024-02-23 | 安徽明天新能源科技有限公司 | Hot-pressing auxiliary reinforced fuel cell membrane electrode and preparation method thereof |
| CN117328099B (en) * | 2023-11-27 | 2024-04-12 | 山东东岳未来氢能材料股份有限公司 | Low-energy-consumption catalytic layer and preparation method thereof |
| CN117577906B (en) * | 2023-12-16 | 2024-05-03 | 杭州质子动力有限公司 | Self-humidifying membrane electrode of air-cooled fuel cell and preparation method thereof |
Citations (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JP2006012676A (en) * | 2004-06-28 | 2006-01-12 | Tomoegawa Paper Co Ltd | Manufacturing method of film stack for membrane-electrode assembly |
| CN101051691A (en) * | 2007-05-14 | 2007-10-10 | 武汉理工大学 | Geo polymer base composite material double pole plate and its preparing method |
| CN101621126A (en) * | 2009-08-13 | 2010-01-06 | 上海交通大学 | Method for preparing fuel cell film pole |
| CN102623717A (en) * | 2012-03-31 | 2012-08-01 | 中国科学院长春应用化学研究所 | Membrane electrode preparation method and membrane electrode |
Family Cites Families (6)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN103078122A (en) * | 2012-12-20 | 2013-05-01 | 华南理工大学 | Self-humidification membrane electrode for proton exchange membrane fuel cell and preparation method thereof |
| CN103531826B (en) * | 2013-10-30 | 2015-12-30 | 中国科学院上海高等研究院 | A kind of method based on sacrificing template structure direct methanol fuel cell nano-porous structure membrane electrode |
| CN106159283A (en) * | 2015-04-08 | 2016-11-23 | 宜兴市四通家电配件有限公司 | A kind of membrane electrode of fuel batter with proton exchange film and preparation method thereof |
| FR3035800B1 (en) * | 2015-05-06 | 2019-10-18 | Commissariat A L'energie Atomique Et Aux Energies Alternatives | CATALYST SUPPORTED BY CARBON NANOTUBES AND GRAPHENE, AND PROCESS FOR PREPARING THE SAME |
| CN105024084A (en) * | 2015-08-19 | 2015-11-04 | 哈尔滨工业大学 | High-temperature proton exchange membrane fuel cell membrane electrode and preparation method thereof |
| CN106784943B (en) * | 2016-12-19 | 2019-05-14 | 华南理工大学 | A kind of membrane electrode of fuel batter with proton exchange film of high power density and preparation method thereof |
-
2016
- 2016-12-19 CN CN201611177018.4A patent/CN106784943B/en active Active
-
2017
- 2017-11-27 WO PCT/CN2017/113215 patent/WO2018113485A1/en active Application Filing
Patent Citations (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JP2006012676A (en) * | 2004-06-28 | 2006-01-12 | Tomoegawa Paper Co Ltd | Manufacturing method of film stack for membrane-electrode assembly |
| CN101051691A (en) * | 2007-05-14 | 2007-10-10 | 武汉理工大学 | Geo polymer base composite material double pole plate and its preparing method |
| CN101621126A (en) * | 2009-08-13 | 2010-01-06 | 上海交通大学 | Method for preparing fuel cell film pole |
| CN102623717A (en) * | 2012-03-31 | 2012-08-01 | 中国科学院长春应用化学研究所 | Membrane electrode preparation method and membrane electrode |
Also Published As
| Publication number | Publication date |
|---|---|
| WO2018113485A1 (en) | 2018-06-28 |
| CN106784943A (en) | 2017-05-31 |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| CN106784943B (en) | A kind of membrane electrode of fuel batter with proton exchange film of high power density and preparation method thereof | |
| Hou et al. | Enhanced low-humidity performance in a proton exchange membrane fuel cell by developing a novel hydrophilic gas diffusion layer | |
| CN101557001B (en) | Fuel cell film electrode and preparation method thereof | |
| JP3922451B2 (en) | Manufacturing method of membrane-electrode-gasket assembly for fuel cell | |
| CN100530797C (en) | Preparation process of membrane electrode of proton exchange membrane fuel cell | |
| CN103358612B (en) | The proton exchange membrane of DMFC and preparation method thereof | |
| US20120107719A1 (en) | Electrode catalyst for membrane electrode of fuel cell and its method of preparation and fuel cell membrane electrode | |
| US20080213644A1 (en) | Solid polyelectrolyte type fuel cell and method of producing the same | |
| CN1988225A (en) | Gas diffusion layer for proton exchanging film fuel cell and its preparing method | |
| CN101000967A (en) | Membrane electrode of protone exchange membrane fuel cell and preparation method thereof | |
| JP2007250274A (en) | Electrode catalyst for fuel cell with enhanced noble metal utilization efficiency, its manufacturing method, and solid polymer fuel cell equipped with this | |
| CN104726891B (en) | Proton exchange membrane water-electrolyzer with internal hydrogen removing function and producing method thereof | |
| CN109065923A (en) | Add the high-performance high power density membrane electrode and preparation method thereof of hydrophily carbon material preparation having from humidifying capacity | |
| CN100407482C (en) | Anti-carbon monoxide composite anode electrode catalyst layer structure and preparation method | |
| CN111584880B (en) | Low-platinum proton exchange membrane fuel cell membrane electrode and preparation method thereof | |
| CN107611452A (en) | A kind of preparation method of the membrane electrode containing three-dimensional hydrophobic cathode catalysis layer | |
| CN103280583A (en) | Method for preparing catalytic layer structure of proton exchange membrane fuel cell | |
| CN103855408B (en) | A kind of membrane electrode improving anode of proton exchange membrane fuel cell water management | |
| CN103531826B (en) | A kind of method based on sacrificing template structure direct methanol fuel cell nano-porous structure membrane electrode | |
| CN100454636C (en) | Making method for core component of water-reservation proton exchange film fuel battery | |
| Liu et al. | Anode catalyst layer with novel microstructure for a direct methanol fuel cell | |
| CN100401563C (en) | Preparation method of membrane electrode commponent of proton exchange membrane fuel cell | |
| CN101140990A (en) | Application of electric pole gaseous diffusion layer in fuel batter with proton exchange film | |
| CN103779582B (en) | A kind of method for preparing fuel cell membrane electrode | |
| CN103367768B (en) | A kind of method preparing double-catalyst-layestructure structure of proton exchange membrane fuel cell |
Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| PB01 | Publication | ||
| PB01 | Publication | ||
| SE01 | Entry into force of request for substantive examination | ||
| SE01 | Entry into force of request for substantive examination | ||
| GR01 | Patent grant | ||
| GR01 | Patent grant |